偏心雙槳攪拌流場(chǎng)及效果分析
[Abstract]:In the production process, polystyrene particles should be suspended and mixed uniformly in liquid styrene, and the solid phase should not be stacked at the bottom and the concentration of solid phase should be uniform. In order to achieve the ideal mixing effect, the effects of eccentricity and rotational speed of the two propellers on the mixing effect are studied in this paper. Taking the bottom elliptical head, the reactor without baffle and the open turbine agitator with double layer 40% discount blade as the research object, the flow field of water stirring and the solid liquid stirring of polystyrene particle and styrene were numerically simulated by Fluent software. The effects of eccentricity and rotational speed on agitation flow pattern, concentration distribution of polystyrene particles and energy consumption were simulated. The (PIV) experiment of particle image velocimetry was used to verify the mixing flow field of water. The results show that eccentricity agitation can increase the velocity of the fluid and restrain the dead zone under the blade effectively, and the increase of eccentricity leads to the increasing deviation of velocity on both sides and the uneven distribution of energy. The concentration distribution of polystyrene particles in eccentrically stirred is more uniform than that in stirring, which can improve the suspending effect of particles in styrene, and the power consumption of the eccentric ratio of 0.15 is 85% of that of the middle stirring under the same stirring effect. The optimum eccentricity and rotation speed are 0.15 and 95 r / min, respectively. At this time, the mixing effect is the best, the distribution of solid concentration is the most uniform, and the power consumption is relatively low.
【作者單位】: 上海應(yīng)用技術(shù)大學(xué)機(jī)械工程學(xué)院;南京工業(yè)大學(xué)機(jī)械與動(dòng)力工程學(xué)院;
【分類號(hào)】:TQ325.2;TQ027.2
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